Paper filler composition

Patent metadata

Field	Value
Publication number	US-2022018068-A1
Application number	US-202117492036-A
Country	US
Kind code	A1
Filing date	Oct 1, 2021
Priority date	May 15, 2009
Publication date	Jan 20, 2022
Grant date	—

Abstract

Methods of preparing partially dried or essentially completely dried compositions comprising microfibrillated cellulose and an inorganic particulate material may include microfibrillating a fibrous substrate comprising cellulose in an aqueous environment by grinding in the presence of an inorganic particulate material to form an aqueous composition comprising microfibrillated cellulose and inorganic particulate material, wherein the fibrous substrate comprising cellulose has a Canadian Standard freeness equal to or less than 450 cm, wherein the fibrous substrate to the inorganic particulate material are in a ratio of about 99.5:0.5 to about 0.5:99.5, and wherein the microfibrillated cellulose has a fibre steepness of from about 20 to about 50; by treating the aqueous composition comprising microfibrillated cellulose and inorganic particulate material to remove at least a portion or substantially all of the water of the aqueous composition to form a partially dried or essentially completely dried composition comprising microfibrillated cellulose and inorganic particulate material.

First claim

1 .- 99 . (canceled)

100 . A method for preparing an aqueous suspension comprising microfibrillated cellulose, the method comprising a step of microfibrillating a fibrous substrate comprising cellulose in an aqueous environment by grinding in the presence of a grinding medium, which is to be removed after completion of grinding and wherein the grinding is carried out in the absence of added grindable inorganic particulate material, wherein the microfibrillated cellulose has a fibre steepness of from about 20 to about 50 and the grinding is performed in a tower mill or a screened grinder, and wherein the grinding medium is present in an amount of at least about 10% by volume of the aqueous environment, and wherein the fibrous substrate comprising cellulose is a recycled pulp, or a papermill broke, or a papermill waste stream, or waste from a papermill, or a combination thereof.

101 . The method according to claim 100 , wherein the tower mill comprises a quiescent zone above one or more grinding zones.

102 . The method according to claim 101 , wherein the tower mill further comprises a classifier above one or more grinding zones, optionally wherein the classifier is a hydrocyclone.

103 . The method according to claim 100 , wherein the grinding is performed under plug flow conditions.

104 . The method according to claim 102 , wherein water is added proximate to the quiescent zone or the classifier to reduce the viscosity of the aqueous suspension comprising microfibrillated cellulose.

105 . The method according to claim 100 , wherein water is added to one or more grinding zones via one or more water injection points located along the length of the tower mill.

106 . The method according to claim 100 , wherein the tower mill comprises a vertical impeller shaft equipped with a series of impeller rotor disks throughout its length.

107 . The method according to claim 100 , wherein the grinding is performed in a screened grinder.

108 . The method according to claim 107 , wherein the screened grinder is a stirred media detritor.

109 . The method according to claim 107 , wherein the screened grinder comprises one or more screen(s) having a nominal aperture size of at least 250 mm.

110 . The method according to claim 108 , wherein the stirred media detritor comprises one or more screen(s) having a nominal aperture size of at least 250 mm.

111 . The method according to claim 100 , wherein the grinding medium is present in an amount up to 70% by volume of the charge.

112 . The method according to claim 100 , wherein the grinding medium comprises particles having an average diameter in the range of from 0.5 mm to 6 mm.

113 . The method according to claim 100 , wherein the grinding medium comprises particles having a specific gravity of at least about 2.5.

114 . The method according to claim 100 , wherein the fibrous substrate comprising cellulose is present in the aqueous environment at an initial solids content of at least 1 wt.

115 . The method according to claim 100 , wherein the fibrous substrate comprising cellulose is present in the aqueous environment at an initial solids content of at least 5 wt.

116 . The method according to claim 100 , wherein the grinding is performed in a cascade of two more grinding vessels.

117 . The method according to claim 100 , wherein the fibrous substrate comprises cellulose having a Canadian Standard freeness equal to or less than 450 cm 3 .

118 . The method according to claim 107 , wherein the fibrous substrate comprises cellulose having a Canadian Standard freeness equal to or less than 450 cm 3 .

119 . The method according to claim 108 , wherein the fibrous substrate comprises cellulose having a Canadian Standard freeness equal to or less than 450 cm 3 .

120 . A method for preparing an aqueous suspension comprising microfibrillated cellulose, the method comprising a step of microfibrillating a fibrous substrate comprising cellulose in an aqueous environment by grinding in the presence of a grinding medium, which is to be removed after completion of grinding, wherein the grinding is carried out in the absence of added grindable inorganic particulate material, wherein the microfibrillated cellulose has a fibre steepness of from about 20 to about 50 and the grinding is performed in a stirred media detritor, wherein the grinding medium is present in an amount of at least about 10% by volume of the aqueous environment, wherein the fibrous substrate comprising cellulose is a recycled pulp, or a papermill broke, or a papermill waste stream, or waste from a papermill, or a combination thereof; and wherein the fibrous substrate comprises cellulose having a Canadian Standard freeness equal to or less than 450 cm 3 .

121 . The method according to claim 120 , wherein the recycled pulp may be dewatered to obtain a wet sheet comprising about 10% solids.

122 . The method according to claim 120 , wherein the recycled pulp may be dewatered to obtain a wet sheet comprising about 15% solids.

123 . The method according to claim 120 , wherein the recycled pulp may be dewatered to obtain a wet sheet comprising about 20% solids.

124 . The method according to claim 120 , wherein the recycled pulp may be dewatered to obtain a wet sheet comprising about 30% solids.

125 . The method according to claim 120 , wherein the recycled pulp may be dewatered to obtain a wet sheet comprising about 40% solids.

Assignees

• Fiberlean Tech Ltd

Inventors

• Husband John Claude
• Svending Per
• Skuse David Robert
• Motsi Tafadzwa

Classifications

• D21C9/001

  Modification of pulp properties (purification D21C9/08) · CPC title

• D21D1/20

  Methods of refining · CPC title

• D21H17/63

  Inorganic compounds · CPC title

• D21B1/30 Primary

  Defibrating by other means · CPC title

• D21H19/385

  Oxides, hydroxides or carbonates · CPC title